Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D1/00—Flotation
  • B03D1/001—Flotation agents
  • B03D1/004—Organic compounds
  • B03D1/012—Organic compounds containing sulfur
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D1/00—Flotation
  • B03D1/001—Flotation agents
  • B03D1/004—Organic compounds
  • B03D1/008—Organic compounds containing oxygen
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C333/00—Derivatives of thiocarbamic acids, i.e. compounds containing any of the groups, the nitrogen atom not being part of nitro or nitroso groups
  • C07C333/14—Dithiocarbamic acids; Derivatives thereof
  • C07C333/18—Esters of dithiocarbamic acids
  • C07C333/26—Esters of dithiocarbamic acids containing any of the groups, X being a hetero atom, Y being any atom, e.g. N-acyldithiocarbamates
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D2201/00—Specified effects produced by the flotation agents
  • B03D2201/02—Collectors
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D2201/00—Specified effects produced by the flotation agents
  • B03D2201/04—Frothers
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D2203/00—Specified materials treated by the flotation agents; Specified applications
  • B03D2203/02—Ores
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D2203/00—Specified materials treated by the flotation agents; Specified applications
  • B03D2203/02—Ores
  • B03D2203/025—Precious metal ores
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P10/00—Technologies related to metal processing
  • Y02P10/20—Recycling

Definitions

• This invention relates generally to froth flotation collectors and froth flotation processes for using the same for the benef ⁇ ciation and recovery of metal values such as copper, lead, zinc, nickel, molybdenum, gold, silver and platinum group metals (PGM), which include platinum and palladium metals, from mineral ore bodies. More particularly, it relates to processes that employ sulfide mineral collectors comprising certain dithiocarbamate compounds which exhibit excellent metallurgical performance over a broad range of pH values.
• PGM platinum group metals
• Froth flotation is a widely used process for benef ⁇ ciating ores containing value minerals.
• a typical froth flotation process involves intermixing an aqueous slurry, which contains finely ground ore particles, with a frothing or foaming agent to produce a froth.
• the ore particles that contain a desired mineral are preferentially attracted to the froth due to an affinity between the froth and the exposed mineral on the surfaces of the ore particles.
• the resulting beneficiated minerals are then collected by separating them from the froth.
• Froth flotation is especially useful for separating finely ground value minerals from their associated gangue or for separating value minerals from one another. Because of the large scale on which mining operations are typically conducted, and the large difference in value between the desired mineral and the associated gangue, even relatively small increases in separation efficiency provide substantial gains in productivity.
• R and R 1 each independently comprise optionally substituted C 1 - 2 0 alkyl, optionally substituted C6- 2 0 aryl, optionally substituted C 2 2 0 alkenyl, or optionally substituted C7-20 aralkyl groups.
• a collector composition for the benef ⁇ ciation of mineral ores comprises at least one dithiocarbamate compound of Formula (I).
• a method is provided for making a dithiocarbamate compound of Formula (I). The method comprises reacting an alkyl or aryl mercaptan of Formula (IV) with an alkoxy or aryloxy carbonyl isothiocyanate of Formula (III) to form the dithiocarbamate compound of Formula (I), where R and R 1 in Formulae (III) and (IV) are defined as in Formula (I) above:
• a method of benef ⁇ ciating a mineral ore comprises forming a slurry comprising particles of the mineral ore.
• the method further comprises intermixing the slurry with an effective amount of a dithiocarbamate compound of Formula (I) to form a froth comprising a plurality of benef ⁇ ciated minerals.
• Embodiments of the present invention provide froth flotation collectors and froth flotation processes utilizing dithiocarbamates of the Formula (I) for the benef ⁇ ciation and recovery of metals from mineral ores.
• metals may include, but are not limited to copper, lead, zinc, nickel, molybdenum, gold, silver and platinum group metals (PGM), including platinum and palladium.
• PGM platinum group metals
• Dithiocarbamates of the Formula (I) may be made in various ways.
• dithiocarbamates of the Formula (I) are made by reacting an alkyl or aryl mercaptan of Formula (IV) with an alkoxy or aryloxy carbonyl isothiocyanate of Formula (III) described above.
• the Examples set forth below describe preferred reaction conditions for making particular dithiocarbamates of the Formula (I).
• Those skilled in the art in view of the guidance provided herein, can identify suitable reaction conditions for making a broad variety of dithiocarbamates of the Formula (I).
• alkoxy or aryloxy carbonyl isothiocyanate of the Formula (III) can be obtained in various ways, e.g., from commercial sources or by methods known to those skilled in the art, see, e.g., Chinese Patent Number 1,548,418 A and U.S. Patent Nos. 4,778,921, 4,659,853, 5,194,673 6,066,754, and 6,184,412.
• the alkoxy or aryloxy carbonyl isothiocyanate of Formula (III) is made by reacting a haloformate of Formula (II) with a thiocyanate salt, where X in Formula (II) is a halogen and R in Formula (II) is defined as in Formula (I) above.
• Thiocyanate salts such as sodium thiocyanate and potassium thiocyanate
• aryl haloformates and alkyl haloformates may be obtained from commercial sources or made by methods known to those skilled in the art.
• alkyl chloroformates can be synthesized by reacting phosgene with the corresponding alkyl mercaptans.
• R and R 1 in Formulae (I) to (IV) each independently comprise optionally substituted C 1-20 alkyl (e.g., C2-6 alkyl), optionally substituted C6-2 0 aryl (e.g., phenyl), optionally substituted C 2 - 20 alkenyl (e.g., allyl), or optionally substituted C 7 _ 2 o aralkyl (e.g., benzyl).
• C 1-20 alkyl e.g., C2-6 alkyl
• optionally substituted C6-2 0 aryl e.g., phenyl
• optionally substituted C 2 - 20 alkenyl e.g., allyl
• optionally substituted C 7 _ 2 o aralkyl e.g., benzyl
• Ci_ 2 o alkyl, C ⁇ - 2 o aryl, C 2 - 2 0 alkenyl and/or C 7 20 aralkyl group may (but need not be) substituted at one or more substitutable positions by one or more groups independently selected from Ci_ 4 alkyl, C 1 - 4 alkoxy, nitro, cyano, halo, Ci_ 4 haloalkyl, amino, Ci_ 4 alkylamino and Ci_ 4 dialkylamino.
• R and R 1 each independently comprise C 1 - 2 0 alkyl, C6- 2 0 aryl, C 2 - 2 0 alkenyl, or C 7 _ 2 o aralkyl.
• R is selected from ethyl, propyl, butyl, allyl, and phenyl.
• R 1 is selected from ethyl, propyl, butyl, pentyl, hexyl, allyl, and phenyl.
• the compound of Formula (I) may be an N-allyloxycarbonyl- S-alkyldithiocarbamate, an N-allyloxycarbonyl-S-aryldithiocarbamate, an N-alkoxycarbonyl- S-allyldithiocarbamate, an N-aryloxycarbonyl-S-allyldithiocarbamate, an N-aryloxycarbonyl- S-alkyldithiocarbamate, or an N-alkoxycarbonyl-S-aryldithiocarbamate.
• R and R 1 are each independently C 2 -6 alkyl.
• the compound of Formula (I) may be an N- alkoxycarbonyl S-ethyl dithiocarbamate, an N-alkoxycarbonyl S-propyl dithiocarbamate, an N-alkoxycarbonyl S-butyl dithiocarbamate, an N-alkoxycarbonyl S-pentyl dithiocarbamate, an N-alkoxycarbonyl S-hexyl dithiocarbamate, an N-ethoxycarbonyl S-alkyl dithiocarbamate, an N-propoxycarbonyl S-alkyl dithiocarbamate, an N-butoxycarbonyl S-alkyl dithiocarbamate, an N-pentoxycarbonyl S-alkyl dithiocarbamate, an N-hexoxycarbonyl S- alkyl dithiocarbamate, or a mixture thereof.
• dithiocarbamates include but are not limited to: N-n- butoxycarbonyl S-n-butyl dithiocarbamate, N-ethoxycarbonyl S-butyl dithiocarbamate, N-butoxycarbonyl S-phenyl dithiocarbamate, N-alloxycarbonyl S-phenyl dithiocarbamate, N- phenoxycarbonyl S-allyl dithiocarbamate, N-ethoxycarbonyl S-phenyl dithiocarbamate, N- ethoxycarbonyl-S-ethyldithiocarbamate, N-propoxycarbonyl-S-ethyldithiocarbamate, N- propoxycarbonyl-S-ethyldithiocarbamate, N-propoxycarbonyl-S-propyldithiocarbamate, N- propoxycarbonyl-S-butyldithiocarbamate, N-propoxycarbonyl-S-but
• An embodiment provides a collector composition for the benef ⁇ ciation of mineral ores, comprising an effective amount of one or more of the dithiocarbamates of the Formula (I) described herein, which may be referred to herein simply as dithiocarbamates.
• a collector composition for the benef ⁇ ciation of mineral ores comprising an effective amount of one or more of the dithiocarbamates of the Formula (I) described herein, which may be referred to herein simply as dithiocarbamates.
• the collector composition used for such benef ⁇ ciation may consist essentially of the dithiocarbamate(s), or may comprise other ingredients, such as diluents (e.g., water, alcohol, oil), pH modifiers, other collectors, frothing agents, etc.
• diluents e.g., water, alcohol, oil
• pH modifiers e.g., sodium bicarbonate
• other collectors include xanthates, xanthogen formates, thiophosphates, thioureas, and dithiocarbamates.
• frothing agents include alcohols (e.g., C ⁇ -8 alkanols such as 2-ethyl hexanol and 4-methyl-2-pentanol, glycols and polyglycols) pine oil, and cresylic acid
• alcohols e.g., C ⁇ -8 alkanols such as 2-ethyl hexanol and 4-methyl-2-pentanol, glycols and polyglycols
• cresylic acid The amount of dithiocarbamate(s) in the collector composition may vary over a broad range, e.g., from about 1% to about 100%, as needed.
• Collector compositions that contain other ingredients in addition to dithiocarbamates of the Formula (I) may be formed prior to intermixing with a mineral slurry or in the presence of the mineral slurry.
• collectors for beneficiation includes the use of collector compositions that consist essentially of the dithiocarbamate(s) described herein and those that further comprise other ingredients, such as the diluents, pH modifiers, other collectors and/or frothing agents referred to above, unless the context indicates otherwise.
• Another embodiment provides a method of beneficiating a mineral ore, comprising forming a slurry comprising mineral ore particles, and intermixing the slurry with an effective amount of the collector composition (comprising or consisting essentially of a compound of Formula (I)) preferably with a frothing agent to form a froth comprising a plurality of benef ⁇ ciated minerals.
• the collector composition comprising or consisting essentially of a compound of Formula (I)
• a frothing agent to form a froth comprising a plurality of benef ⁇ ciated minerals.
• sulfide and/or oxide metal and mineral values are recovered by froth flotation methods in the presence of a collector composition as described herein.
• these collector compositions provide enhanced beneficiation of sulfide mineral values from base metal sulfide ores over a wide range of pH values and, more preferably, under slightly acidic, neutral, and slightly alkaline conditions.
• this class of collector compositions may provide significant improvements in the recovery of metals over conventional collectors, such as thionocarbamates.
• the ore particles in the slurry are preferably made by size- reducing the ore to provide ore particles of flotation size, in a manner generally known to those skilled in the art.
• the ore can be crushed to about - 10 mesh size followed by wet grinding in a steel ball mill to the desired mesh size.
• pebble milling may be used.
• the particle size to which a particular ore is size-reduced in order to liberate mineral values from associated gangue or non-values, i.e., liberation size typically varies from ore to ore and may depend on a number of factors. These factors may include, but are not limited to, the geometry of the mineral deposits within the ore, such as striations, agglomeration, and comatrices.
• Determination that particles have been size-reduced to the desired liberation size may be made by microscopic examination using methods known to those skilled in the art.
• suitable particle sizes may vary from about 50 mesh to about 400 mesh.
• the ore is size-reduced to provide flotation sized particles in the range of about +65 mesh to about -200 mesh.
• base metal sulfide ores are size-reduced to provide from about 10% to about 40%, preferably from about 14% to about 30% by weight of particles of +100 mesh and from about 40% to about 80%, preferably from about 45% to about 75% by weight of particles of -200 mesh sizes.
• a slurry comprising the mineral ore particles may be formed in various ways known to those skilled in the art. Examples of slurry formation may include, but are not limited to, intermixing liberation-sized ore particles with water and by grinding the ore in the presence of water.
• the pH of the slurry may be adjusted at any stage in the slurry formation process.
• a pH modifier such as an acid or base is added to the slurry or to the grind during size reduction, in order to provide the slurry with a selected pH.
• the pH modifiers include sulfuric acid, sodium carbonate and lime.
• good beneficiation may be obtained at pulp slurry pH values in the range of about 1 to about 12, and particularly in the pH range of from about 5 to about 10.5.
• the pH of the slurry may be adjusted at any point in the process of preparing the ore for froth flotation or during the froth flotation process itself.
• the slurry of mineral ore particles preferably contains an amount of water effective to provide from about 10% to about 60% pulp solids, more preferably from about 25% to about 50% pulp solids, and most preferably from about 30% to about 40% pulp solids, by weight based on the total slurry weight.
• the flotation of sulf ⁇ de-containing minerals is performed.
• such minerals include those that comprise metals that may include, but are not limited to, copper, nickel, molybdenum, lead, zinc, gold, silver and platinum group (PGM) metals.
• Flotation may be performed at a pH in the range of about 1 to about 12, preferably from about 6 to about 12 and more preferably about 9 to about 11.5.
• the slurry is preferably conditioned by intermixing it with effective amounts of a frothing agent and a collector composition (preferably comprising at least one dithiocarbamate of the Formula (I)) to form a froth containing benef ⁇ ciated sulfide minerals.
• the frothing agent, collector and slurry may be intermixed in any order.
• the collector may be added to the slurry and/or to the grind in accordance with conventional methods.
• effective amount it is meant any amount of the respective components which provides a desired level of beneficiation of the desired metal values.
• Any frothing agent known to those skilled in the art may be employed in the froth flotation process.
• suitable frothing agents include: straight or branched chain low molecular weight hydrocarbon alcohols, such as C ⁇ _8 alkanols, 2-ethyl hexanol and 4-methyl-2-pentanol (also known as methyl isobutyl carbinol or MIBC), as well as pine oils, cresylic acid, glycols, polyglycols, and combinations thereof.
• Typical amounts of frothing agent are in the range of about 0.01 to about 0.2 pound of frothing agent per ton of ore treated, although higher or lower amounts of frothing agent may be effective in particular situations.
• the collector compositions described herein may be used alone, in combination with one another, and/or in combination with one or more second collectors, e.g., another sulfide mineral collector.
• second collectors include, but are not limited to xanthates, xanthogen formates, thiophosphates, thioureas, and/or dithiocarbamates, e.g., dialkyldithiocarbamates.
• a collector composition (preferably comprising a dithiocarbamate of the Formula (I)) is intermixed with a frothing agent and pulp slurry in amounts ranging from about 0.005 to about 5 pounds of the collector per ton of ore in the slurry, preferably about 0.1 Ib. to about 2 lbs./ton and more preferably .01 Ib to about 1 lb/ton, on same basis.
• the collector is preferably used in amounts of from about 0.01 lbs./ton to about 5 lbs./ton of ore in the slurry.
• Routine experimentation in accordance with conventional froth flotation methods may be utilized to determine suitable conditions to float the desired sulfide mineral values in the froth concentrate and, preferably, selectively reject or depress pyrite and other gangue sulfides.
• suitable conditions to float the desired sulfide mineral values in the froth concentrate and, preferably, selectively reject or depress pyrite and other gangue sulfides.
• pyrite arsenopyrite, galena, sphalerite and a variety of other metal sulfides along with the above mentioned valeue metals.
• the collector compositions e.g., dithiocarbamates of the
• Formula (I) are generally easily dispersible in the mineral pulp.
• these collectors when added to a flotation cell, these collectors typically provide higher metals recovery, as shown in the examples provided below.
• the collector compositions may be used to selectively concentrate or collect certain metal value sulfides, particularly those of gold, copper, molybdenum, PGM, lead, and zinc, from other gangue sulfides, e.g., pyrite and pyrrhotite, and other gangue materials, e.g., silicates, carbonates, etc.
• collectors may also be used in situations in which it is desirable to collect substantially all of the sulfides in an ore, including sphalerite (ZnS) and the iron sulfides, e.g., pyrite and pyrrhotite, in addition to the principal sulfide minerals.
• ZnS sphalerite
• the iron sulfides e.g., pyrite and pyrrhotite
• n-butyl mercaptan Approximately 20 mL of n-butyl mercaptan is added to about 10 grams of n- butoxycarbonyl isothiocyanate.
• n-Butoxycarbonyl isothiocyanate is produced by the procedures described in U.S. Patent Numbers 4,778, 921 and 5,194,673, which are hereby incorporated by reference in their entireties.
• the reaction is substantially exothermic, with the temperature rising from about 25 to 6O 0 C.
• Example 2 The general procedure of Example 1 is utilized, employing phenyl mercaptan and alloxycarbonyl isothiocyanate..
• Example 2 The general procedure of Example 1 is used, employing allyl mercaptan and phenoxycarbonyl isothiocyanate.
• Example 2 The general procedure of Example 1 is used, employing phenyl mercaptan and ethoxycarbonyl isothiocyanate.
• Example 1 The general procedure of Example 1 is used, employing phenyl mercaptan and butoxycarbonyl isothiocyanate. The final product, N-butoxycarbonyl S-phenyl dithiocarbamate, possesses melting point of about 71-73°C. Examples 7-12 - Recovery of metal values using NBCNBDTS and NBCNBTC
• An ore body containing copper (Cu), molybdenum (Mo), and gold (Au) values is beneficiated by froth flotation.
• the flotation parameters for each test are as follows: approximately 2200g/ton of lime, approximately 30g/ton of a roughly 3 : 1 mixture of Oreprep501/Oreprep507 frothers (Cytec Industries, Inc., West Patterson, NJ), where pulp solids are approximately 67%, and the collectors are added to the mill.
• the recoveries (Rec.) of each of the metal values are reported in Table 1 using an N-n-butoxycarbonyl S-n-butyl dithiocarbamate (NBCNBDTS) collector of the present invention and an N-n- butoxycarbonyl-O-n-butyl thionocarbamate (NBCNBTC) collector used in conventional practices.
• Values of pH, dosage per ton of pulp solids, and grind time are varied in Examples 7-12.
• Table 1 illustrates that the NBCNBDTS collector of the present invention improve recovery over the conventional NBCNBTC collector.
• Examples 7/7C and 8/8C benef ⁇ ciation parameters of about pH 9.5, grind time about 6.5 min, and dosages of about 4g/ton and about 8g/ton (based on tons of solids in slurry) are utilized. It is observed that with a dosage of about 4 grams per ton, the NBCNBDTS recovers a greater percentage of Au, Cu, and Mo than NBCNBTC. When the dosage is increased to about 8g/ton, the collectors exhibit approximately constant recovery rates. It is further observed that the recovery percentage at low dose is greater than the conventional NBCNBTC at the higher dose. Thus, the NBCNBDTS may be used in smaller dosages than the conventional NBCNBTC, providing a cost savings per unit metal recovered.
• Examples 9/9C and 10/lOC benef ⁇ ciation parameters of about pH 9.5, grind time about 5.0 min, and dosages of about 4g/ton and about 8g/ton are used. At both 4g/ton and 8g/ton dosages, the NBCNBDTS recovers a greater percentage of Au, Cu, and Mo than NBCNBDTS.
• Examples 11/11C and 12/12C beneficiation parameters of about pH 10.5, grind time about 5.0 min, and dosages of about 4g/ton and 8g/ton are used. Again, using both the 4g/ton and 8g/ton dosages, the NBCNBDTS recovers a greater percentage of Au, Cu, and Mo than NBCNBDTS.
• the flotation parameters for each test are as follows: approximately 2 kg of ore is used; pH of pulp is -8.6; approximately 15g/ton of Betafroth 206 (Betachem (Pty) Ltd, South Africa) is used as frother; ore is ground to 70% -200 mesh at 67% solids; the collectors are added at 20g/t to the mill and two stages of flotation in the proportion 10:5:5; conditioning times for reagents are typically 2 min. and total flotation time is 15 min.; and guar gum is used at 40 g/t as a depressant for talc.
• the flotation parameters for each test are as follows: approximately 0.5 kg of ore is used; 1.36 kg/t of lime is added to the mill to provide a pulp pH of -9.3; approximately 26g/ton of DOWFROTH 250 (Dow Chemical, Midland, MI, USA) is used as frother added in two stages of flotation in the proportion of 16: 10; ore is ground to 55% -200 mesh at 67% solids; the collectors are added at 8g/t to the mill; conditioning time in the cell is typically 2 min.
• NBCNBDTS N-n-Butoxycarbonyl S-n-butyl Dithiocarbamate
• NiBCNBDTS N-iso-Butoxycarbonyl S-n-butyl Dithiocarbamate
• NBCNBTC N-n-butoxycarbonyl O-n-Butyl Thionocarbamate
• the flotation parameters for each test are as follows: approximately 1 kg of ore is used; 200 g/t of lime is added to the mill to provide a pulp pH of -9.5; approximately 20g/ton of Methyl Isobutyl Carbinol (MIBC) is used as a frother added in two stages of flotation in the proportion of 15:5; ore is ground to 18% +100 mesh at 67% solids; the collectors are added at 5 g/t to the mill and second stage of flotation in the proportion of 3:2; conditioning time with reagents is 2 min.
• MIBC Methyl Isobutyl Carbinol
• the flotation parameters for each test are as follows: approximately 1.1 kg of ore is used; 1.2 kg/t of lime is added to the mill to provide a pulp pH of ⁇ 10; approximately 12g/ton of a 5:3 ration mixture of AEROFROTH 76A and Oreprep X- 133 (Cytec Industries Inc., West Paterson, NJ, USA) is used as frother added in two stages of flotation in the proportion of 8:4; ore is ground to 20% +100 mesh at 55% solids; the collectors are added at 1 lg/t to the mill and second stage of flotation in the proportion of 6:5; conditioning time with reagents is 1 min.
• An ore body containing principally gold (Au) as the primary value metal associated with a variety of sulfide minerals - including pyrite, arsenopyrite, galena, chalcopyrite, tennantite, tetrahedrite, sphalerite and minor amounts of other sulfides - is beneficiated by froth flotation to recover Au and other value metals.
• An additional industry need for this type of primary gold ores is to maximize the recovery of all sulfide minerals (expressed as Total Sulfur Recovery).
• the flotation parameters for each test are as follows: approximately 0.5 kg of ore is used; pulp pH is -8.5; approximately 40g/ton of a 1 :3 ratio mixture of Oreprep 501/Oreprep 507 (Cytec Industries Inc., West Paterson, NJ) is used as a frother added in two stages of flotation in the proportion of 10: 10; ore is ground to 78% -200 mesh at 50% solids; the collectors are added at 50g/t to the mill and third stage of flotation in the proportion of 25:25; potassium amyl xanthate (PAX) is used as a secondary collector at 75g/t added to mill and third stage of flotation in the proportion of 38:37; a carbon collector Reagent S-7944 (Cytec Industries Inc., West Paterson, NJ) is added to the mill at 50 g/t to float carbonaceous matter in the first stage of flotation; conditioning time with reagents is 2 min.
• Example 30 An ore body similar to the one used for Example 30 and from the same mine is used in this example. The objective is similar to that in Example 30 - to maximize the recovery of Au values and all the associated sulfide minerals (expressed as Total Sulfur Recovery).
• pulp pH is ⁇ 10.1; approximately 40g/ton of a 1 :3 ratio mixture of Oreprep 501/Oreprep 507 (Cytec Industries Inc., West Paterson, NJ) is used as a frother added in three stages of flotation in the proportion of 30:5:5; ore is ground to 73% -200 mesh at 67% solids; the collectors are added at 50g/t to the second and third stage of flotation in the proportion of 2: 1; potassium amyl xanthate (PAX) is used as a secondary collector at 75g/t added to second and third stages of flotation in the proportion of 2: 1; a carbon collector Reagent S-7944 (Cytec Industries Inc., West Paterson, NJ) is added to the mill at 50 g/t to float carbonaceous matter in the first stage of flotation; conditioning time with reagents is 2 min.
• pulp pH is ⁇ 10.1
• NiBCNBDTS N-iso-Butoxycarbonyl S-n-butyl Dithiocarbamate
• NiBCiBTC N-iso-butoxycarbonyl O-iso-Butyl Thionocarbamate
• DIBDTPI Sodium Diisobutyl Dithiophosphinate
• NaEX Sodium Ethyl Xanthate
• Ni principally nickel
• magnesium silicates which adversely affect Ni recoveries.
• the flotation parameters for each test are as follows: approximately 0.5 kg of ore is used; 6kg/t of sodium carbonate is added to the mill to provide a flotation pH of -9.3; approximately 30g/ton of triethoxybutane is used as a frother added in the first stage of flotation; ore is ground to 65% -200 mesh at 66% solids; collector of present invention or the corresponding comparative thionocarbamate is added at 7.5g/t to the mill; sodium ethyl xanthate (NaEX) at 15 g/t and sodium diisobutyl dithiophosphinate (DIBDTPI) at 7.5g/t are used as secondary collectors, both added to the mill; conditioning time with reagents is 1 min.
• the flotation parameters for each test are as follows: approximately 0.5 kg of ore; 1.36 kg/t of lime is added to the mill to provide a pulp pH of -9.3; approximately 26g/ton of DOWFROTH 250 (Dow Chemical, Midland, MI, USA) is used as frother added in two stages of flotation in the proportion of 16: 10; ore is ground to 55% -200 mesh at 67% solids; the collectors are added at 8g/t to the mill; conditioning time in the cell is typically 2 min. and total flotation time is 7 min.; and flotation conducted at approximately 34% solids in three stages.
• the recoveries (Rec.) of each of the metal values (Ni and Cu) are reported in Table 9 as Examples 33-46.

Landscapes

• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Manufacture And Refinement Of Metals (AREA)
• Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
• Agricultural Chemicals And Associated Chemicals (AREA)
• Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Priority Applications (12)

Applications Claiming Priority (2)

Publications (2)

Family

ID=39358119

Family Applications (1)

Country Status (20)

Cited By (1)

Families Citing this family (27)

Citations (13)

Family Cites Families (11)

• 2008
  • 2008-01-21 CA CA2676312A patent/CA2676312C/en active Active
  • 2008-01-21 RU RU2009133343/03A patent/RU2455077C2/ru not_active IP Right Cessation
  • 2008-01-21 DK DK08713850.9T patent/DK2117718T3/en active
  • 2008-01-21 PL PL08713850T patent/PL2117718T3/pl unknown
  • 2008-01-21 JP JP2009549160A patent/JP5566113B2/ja not_active Expired - Fee Related
  • 2008-01-21 UA UAA200909123A patent/UA102373C2/ru unknown
  • 2008-01-21 AP AP2009004943A patent/AP2526A/xx active
  • 2008-01-21 CN CN200880004363.5A patent/CN101605608B/zh not_active Expired - Fee Related
  • 2008-01-21 ES ES08713850.9T patent/ES2637138T3/es active Active
  • 2008-01-21 CN CN201310338287.4A patent/CN103433145B/zh not_active Expired - Fee Related
  • 2008-01-21 EP EP08713850.9A patent/EP2117718B1/en active Active
  • 2008-01-21 BR BRPI0807194-2A patent/BRPI0807194A2/pt not_active Application Discontinuation
  • 2008-01-21 WO PCT/US2008/051537 patent/WO2008097707A1/en active Application Filing
  • 2008-01-21 PT PT87138509T patent/PT2117718T/pt unknown
  • 2008-01-21 AU AU2008214151A patent/AU2008214151B2/en not_active Ceased
  • 2008-02-04 CL CL200800340A patent/CL2008000340A1/es unknown
  • 2008-02-05 PE PE2008000246A patent/PE20081413A1/es active IP Right Grant
  • 2008-02-05 AR ARP080100483A patent/AR065186A1/es active IP Right Grant
  • 2008-02-07 US US12/027,334 patent/US8376142B2/en active Active
• 2009
  • 2009-07-27 ZA ZA2009/05233A patent/ZA200905233B/en unknown
• 2014
  • 2014-05-16 JP JP2014102205A patent/JP5856649B2/ja not_active Expired - Fee Related
• 2017
  • 2017-01-05 AR ARP170100031A patent/AR107307A2/es unknown
  • 2017-08-10 CY CY20171100864T patent/CY1119565T1/el unknown

Patent Citations (13)

Non-Patent Citations (15)

Also Published As

Similar Documents

Legal Events